PROCESS AND PLANT FOR REFINING OIL-CONTAINING SOLIDS
    2.
    发明申请
    PROCESS AND PLANT FOR REFINING OIL-CONTAINING SOLIDS 审中-公开
    精炼含油固体的工艺和设备

    公开(公告)号:WO2009010157A3

    公开(公告)日:2009-04-09

    申请号:PCT/EP2008005078

    申请日:2008-06-24

    Abstract: For refining oil-containing solids, in particular oil sand or oil shale, there is proposed a process with the following steps: supplying the oil-containing solids to a reactor and expelling an oil- containing vapor at a temperature of 300 to 1000 °C, - supplying the oil-containing vapor expelled in the reactor to a cracker, in which the heavy oil components are broken down, separating the products obtained in the cracker and withdrawing the product streams, introducing the solids left in the reactor including the unevaporated fraction of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500 °C, preferably 1050 to 1200 °C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by a blocking device.

    Abstract translation: 为了精炼含油固体,特别是油砂或油页岩,提出了一种具有以下步骤的方法:将含油固体供应到反应器并在300-1000℃的温度下排出含油蒸汽 将在反应器中排出的含油蒸气供应到裂化器中,其中重油组分被分解,分离裂化器中获得的产物并抽出产物流,引入包含未蒸发部分的反应器中残留的固体 的重质烃进入炉中,在600至1500℃,优选1050至1200℃的温度下将留在炉中固体中的重质烃燃烧,将热固体从炉再循环到反应器中,其中氧化气氛 通过阻挡装置将炉与反应器的气氛分离。

    PROCESS AND PLANT FOR REFINING OIL-CONTAINING SOLIDS
    5.
    发明申请
    PROCESS AND PLANT FOR REFINING OIL-CONTAINING SOLIDS 审中-公开
    精炼含油固体的工艺和设备

    公开(公告)号:WO2009010157A8

    公开(公告)日:2010-04-22

    申请号:PCT/EP2008005078

    申请日:2008-06-24

    Abstract: For refining oil-containing solids, in particular oil sand or oil shale, there is proposed a process with the following steps: supplying the oil-containing solids to a reactor and expelling an oil- containing vapor at a temperature of 300 to 1000 °C, - supplying the oil-containing vapor expelled in the reactor to a cracker, in which the heavy oil components are broken down, separating the products obtained in the cracker and withdrawing the product streams, introducing the solids left in the reactor including the unevaporated fraction of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500 °C, preferably 1050 to 1200 °C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by a blocking device.

    Abstract translation: 为了精炼含油固体,特别是油砂或油页岩,提出了一种具有以下步骤的方法:将含油固体供应到反应器并在300-1000℃的温度下排出含油蒸汽 将在反应器中排出的含油蒸气供应到裂化器中,其中重油组分被分解,分离裂化器中获得的产物并抽出产物流,引入包含未蒸发部分的反应器中残留的固体 的重质烃进入炉中,在600至1500℃,优选1050至1200℃的温度下将留在炉中固体中的重质烃燃烧,将热固体从炉再循环到反应器中,其中氧化气氛 通过阻挡装置将炉与反应器的气氛分离。

    PROCESS FOR PLANT FOR REFINING RAW MATERIALS CONTAINING ORGANIC CONSTITUENTS
    6.
    发明申请
    PROCESS FOR PLANT FOR REFINING RAW MATERIALS CONTAINING ORGANIC CONSTITUENTS 审中-公开
    用于精炼含有机原料的工厂的工艺

    公开(公告)号:WO2009100840A3

    公开(公告)日:2010-02-25

    申请号:PCT/EP2009000729

    申请日:2009-02-04

    CPC classification number: B01J8/1818 B01J2208/00752 C10G1/02

    Abstract: In accordance with the invention, refining raw materials containing organic constituents, such as solids containing oil and/or bitumen, in particular oil or tar sand or oil shale, is effected with the following steps: - supplying the raw materials to a reactor and expelling fuel gases at a temperature of about 300 to 1000°C, preferably about 500 to 800°C, introducing the solids left in the reactor including the non-evaporated fractions of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500°C, preferably 700 to 900°C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by means of a blocking device.

    Abstract translation: 根据本发明,包含含有机油成分的原料,例如含有油和/或沥青的固体,特别是油或焦油砂或油页岩的原料,是通过以下步骤进行的: - 将原料供应到反应器并排出 将温度在约300至1000℃,优选约500至800℃的燃料气体引入包含非蒸发馏分的重质烃的反应器中的固体进入炉中,将残留在固体中的重质烃燃烧 该炉在600至1500℃,优选700至900℃的温度下,将来自炉的热固体再循环到反应器中,其中通过阻塞装置将炉的氧化气氛与反应器的气氛分离 。

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